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• S <br /> Technical Description <br /> The different materials are always different specific gravities and are usually made up of various sizes <br /> M of gravel,garnet, sand, and anthracite coal. The-denser filter media are placed below the coarser but <br /> L less dense coal, thus allowing deeper penetration in the direction of flow and maintaining a coarse <br /> surface layer even after backwash. This filter media design concept is termed multimedia. <br /> BODS concentrations that are trapped in the suspended solids of the secondary effluent can be <br /> effectively removed in a well-designed tertiary filter;however,standard multimedia filtration has little <br /> or no measurable effect on the removal of soluble BOD which is generally 10 microns or less in size. <br /> In applications where extreme effluent polishing is required, super or microfilters may be added after <br /> the multimedia filter. Even a reverse-osmosis (RO) system may be used as a final filter. <br /> RO in conjunction with microfilters is at a state in technological development where it is possible to <br /> remove particulates down to 0.1 micron or 0.00000394 inch, although it is very unlikely the need for <br /> this type of filtration will ever be required in the wastewater treatment and reclamation area. <br /> The most important consideration in the sizing of tertiary filters, and one requiring considerable <br /> engineering judgment, is selection of the application rate, which is expressed as gallons per minute <br /> applied per square foot of filter surface area. <br /> In many cases, the maximum application rate is fixed by a regulatory agency. Some factors that must <br /> be considered in selection of the rate of application include: 1) efficiency of the secondary treatment <br /> process;2) flow pattern and; 3) filter cycle duration and backwash water production; 4) capital cost <br /> of equipment. <br /> With the Bio-Pure system, designed-in plant flow equalization allows filter flow rate selections based <br /> on equalized flow rates, which removes the problems that result from periodic surge flows. <br /> With the unique batch design of the Bio-Pure secondary process, daily flow patterns(as well as peak <br /> flow rates) are near constant, thus a set schedule can be maintained for backwashing the filter media <br /> during low system flow periods. <br /> ELECTRONICIELECTRICAL CONTROL SYSTEM <br /> The Bio-Pure system control unit provided by AquaClear manages the operational functions of the <br /> entire treatment system with solid-state memory. The memory is programmed at the factory and is <br /> retained in the program controller (PC) by either a battery backup or an EPROM. The memory <br /> L consists of firmware located within the solid-state assembly. <br /> a <br /> In addition to the PC are solid-state relays,circuit breakers, a discharge flow counter, and a settling <br /> time totalizer. <br /> Start/stop cycles of individual pumps are preprogrammed into.the microprocessor. These cycles are <br /> based upon pumping and settling times and are initially set at the factory. Actual field operation times <br /> may vary; thus, provisions are made for reprogramming the microprocessor in the field. <br /> All pump cycles are protected from memory loss by standby battery or by the EPROM,which retains <br /> the program memory during periods of electricalinterruptions. <br /> 18 <br />